Chemical Properties of Butane, 1-(ethenyloxy)- (CAS 111-34-2)

InChI

InChI=1S/C6H12O/c1-3-5-6-7-4-2/h4H,2-3,5-6H2,1H3

InChI Key

UZKWTJUDCOPSNM-UHFFFAOYSA-N

Formula

C6H12O

SMILES

C=COCCCC

Molecular Weight¹

100.16

CAS

111-34-2

Other Names

• 1-(ETHYNYLOXY)BUTANE
• 1-(Ethenyloxy)butane
• 1-(Vinyloxy)-butane
• 1-(vinyloxy)butane
• 1-Butoxyethylene
• 1-vinyloxybutane
• BUTOXYETHENE
• BVE
• Butoxyethylene
• Butyl vinyl ether
• Ethenyl n-butyl ether
• Ether, butyl vinyl
• NSC 8264
• VINYL N-BUTYL ETHER
• Vinyl butyl ether
• n-Butyl vinyl ether
• n-C4H9OCH=CH2

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3954		Relay (1.0) Calculated Property
ΔcH°liquid	[-3860.20; -3857.00]	kJ/mol
ΔcH°liquid	-3860.20 ± 1.10	kJ/mol	NIST
ΔcH°liquid	-3857.00 ± 0.80	kJ/mol	NIST
ΔfG°	-17.52	kJ/mol	Joback Calculated Property
ΔfH°gas	[-182.40; -179.20]	kJ/mol
ΔfH°gas	-179.20 ± 1.20	kJ/mol	NIST
ΔfH°gas	-182.40	kJ/mol	NIST
ΔfH°liquid	[-219.00; -215.80]	kJ/mol
ΔfH°liquid	-215.80 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-219.00 ± 0.80	kJ/mol	NIST
ΔfusH°	11.20	kJ/mol	Joback Calculated Property
ΔvapH°	31.75	kJ/mol	Relay (1.0) Calculated Property
IE	8.90	eV	Relay (1.0) Calculated Property
log10WS	-1.89		Relay (1.0) Calculated Property
logPoct/wat	1.947		Crippen Calculated Property
McVol	96.970	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
NFPA Safety	2		KDB
Pc	3200.00 ± 250.00	kPa	NIST
ρc	261.11 ± 12.02	kg/m3	NIST
Inp	[671.00; 695.00]
Inp	695.00		NIST
Inp	671.00		NIST
Inp	679.00		NIST
Inp	687.00		NIST
Inp	695.00		NIST
I	858.00		NIST
Tboil	[366.00; 367.10]	K
Tboil	367.00	K	NIST
Tboil	366.00	K	NIST
Tboil	367.10	K	NIST
Tc	540.50 ± 2.00	K	NIST
Tfus	172.22	K	Relay (1.0) Calculated Property
Vc	0.358	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[168.37; 221.32]	J/mol×K	[355.78; 523.68]
Cp,gas	168.37	J/mol×K	355.78	Joback Calculated Property
Cp,gas	177.92	J/mol×K	383.76	Joback Calculated Property
Cp,gas	187.18	J/mol×K	411.75	Joback Calculated Property
Cp,gas	196.15	J/mol×K	439.73	Joback Calculated Property
Cp,gas	204.82	J/mol×K	467.71	Joback Calculated Property
Cp,gas	213.21	J/mol×K	495.69	Joback Calculated Property
Cp,gas	221.32	J/mol×K	523.68	Joback Calculated Property
Cp,liquid	231.80	J/mol×K	298.15	NIST
η	[0.0002123; 0.0029205]	Pa×s	[177.85; 355.78]
η	0.0029205	Pa×s	177.85	Joback Calculated Property
η	0.0013807	Pa×s	207.51	Joback Calculated Property
η	0.0007872	Pa×s	237.16	Joback Calculated Property
η	0.0005086	Pa×s	266.81	Joback Calculated Property
η	0.0003585	Pa×s	296.47	Joback Calculated Property
η	0.0002694	Pa×s	326.12	Joback Calculated Property
η	0.0002123	Pa×s	355.78	Joback Calculated Property
ΔvapH	[29.60; 36.10]	kJ/mol	[318.50; 367.10]
ΔvapH	36.10	kJ/mol	318.50	NIST
ΔvapH	35.20 ± 0.20	kJ/mol	357.00	NIST
ΔvapH	32.50 ± 0.20	kJ/mol	357.00	NIST
ΔvapH	29.60 ± 0.20	kJ/mol	357.00	NIST
ΔvapH	31.58	kJ/mol	367.10	NIST
ρl	[758.80; 780.20]	kg/m3	[298.15; 313.15]
ρl	780.20	kg/m3	298.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl	769.00	kg/m3	303.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρl	774.10	kg/m3	303.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl	763.90	kg/m3	308.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρl	768.20	kg/m3	308.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl	758.80	kg/m3	313.15	Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
ρl	763.30	kg/m3	313.15	Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.62]	kPa	[274.58; 389.11]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.54615e+01
Coefficient B			-3.51136e+03
Coefficient C			-4.31680e+01
Temperature range, min.			274.58
Temperature range, max.			389.11
Pvap	1.33	kPa	274.58	Calculated Property
Pvap	2.94	kPa	287.31	Calculated Property
Pvap	6.00	kPa	300.03	Calculated Property
Pvap	11.43	kPa	312.76	Calculated Property
Pvap	20.57	kPa	325.48	Calculated Property
Pvap	35.17	kPa	338.21	Calculated Property
Pvap	57.53	kPa	350.93	Calculated Property
Pvap	90.49	kPa	363.66	Calculated Property
Pvap	137.51	kPa	376.38	Calculated Property
Pvap	202.62	kPa	389.11	Calculated Property
Pvap	[1.31e-04; 3086.33]	kPa	[181.15; 536.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.18610e+01
Coefficient B			-7.10617e+03
Coefficient C			-9.96430e+00
Coefficient D			7.13053e-06
Temperature range, min.			181.15
Temperature range, max.			536.00
Pvap	1.31e-04	kPa	181.15	Calculated Property
Pvap	0.02	kPa	220.58	Calculated Property
Pvap	0.67	kPa	260.01	Calculated Property
Pvap	7.05	kPa	299.43	Calculated Property
Pvap	38.90	kPa	338.86	Calculated Property
Pvap	141.40	kPa	378.29	Calculated Property
Pvap	387.84	kPa	417.72	Calculated Property
Pvap	875.73	kPa	457.14	Calculated Property
Pvap	1725.20	kPa	496.57	Calculated Property
Pvap	3086.33	kPa	536.00	Calculated Property

Similar Compounds

Find more compounds similar to Butane, 1-(ethenyloxy)-.

Mixtures

• Acetic acid ethenyl ester + Butane, 1-(ethenyloxy)-
• Butane, 1-(ethenyloxy)- + Acetic acid, hexyl ester

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
• Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.